WO2007137847A1 - Procédé de production d'une composition vaccinale - Google Patents

Procédé de production d'une composition vaccinale Download PDF

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Publication number
WO2007137847A1
WO2007137847A1 PCT/EP2007/004819 EP2007004819W WO2007137847A1 WO 2007137847 A1 WO2007137847 A1 WO 2007137847A1 EP 2007004819 W EP2007004819 W EP 2007004819W WO 2007137847 A1 WO2007137847 A1 WO 2007137847A1
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WIPO (PCT)
Prior art keywords
volume
aqueous phase
antigen
vaccine composition
aluminium
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PCT/EP2007/004819
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English (en)
Inventor
Bernd Fiedler
Roland Weyhenmeyer
Karl Melber
Zbigniew Janowicz
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Rhein Biotech Gesellschaft für neue Biotechnologische Prozesse und Produkte mbH
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Publication of WO2007137847A1 publication Critical patent/WO2007137847A1/fr

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    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K39/00—Medicinal preparations containing antigens or antibodies
    • A61K39/12—Viral antigens
    • A61K39/29—Hepatitis virus
    • A61K39/292—Serum hepatitis virus, hepatitis B virus, e.g. Australia antigen
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K39/00—Medicinal preparations containing antigens or antibodies
    • A61K39/12—Viral antigens
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K39/00—Medicinal preparations containing antigens or antibodies
    • A61K2039/555—Medicinal preparations containing antigens or antibodies characterised by a specific combination antigen/adjuvant
    • A61K2039/55505—Inorganic adjuvants
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N2730/00—Reverse transcribing DNA viruses
    • C12N2730/00011—Details
    • C12N2730/10011—Hepadnaviridae
    • C12N2730/10111—Orthohepadnavirus, e.g. hepatitis B virus
    • C12N2730/10134—Use of virus or viral component as vaccine, e.g. live-attenuated or inactivated virus, VLP, viral protein

Definitions

  • the present invention relates to a process for production of a vaccine composi ⁇ tion, the vaccine composition obtainable by this process, a vaccine composition comprising a substrate and an antigen, and the use of a vaccine composition.
  • Vaccine compositions for prevention of viral illnesses for example for prevention of a hepatitis B infection, are known from the prior art.
  • EP-A-O 576 478 describes a vaccine composition based on aluminium salt particles, on whose surface an antigen as well as 3-0-deacetylated monophos- phoryl lipid A (3D-MPL), have been absorbed.
  • EP-A-O 689 454 and EP-A-O 633 784 describe a process for production of a vaccine composition, in which first an antigen and then a 3D-MPL as adjuvant are absorbed on the surface of an aluminium salt particle.
  • the vaccine compositions described in these European patent applications are characterised in that the adjuvant and the antigen are at least partially immobilised in the same aluminium salt particles.
  • WO-A-00/23105 describes an adjuvant composition comprising immune stimulants, which are absorbed at the surface of a metal salt particle, whereby the metal salt particle is substantially free from other antigens.
  • the adjuvant compositions described in this state of the art are obtained in that first the adjuvant is immobi- Used at the surface of an aluminium salt particle and, separately, the antigen is immobilised on the surface of another aluminium salt particle. In order to complete the vaccine composition, the aluminium salt particles are then combined which each other.
  • the vaccine composition described in this international patent application is, accordingly, characterised in that the adjuvant and antigen are im- mobilised on different aluminium salt particles.
  • the disadvantage of the vaccine compositions known from the state of the art consists in that, inter alia, they are characterised by a poor stability.
  • This poor stability of the vaccine compositions consisting of the three components aluminium salt particle, antigen and adjuvant expresses itself, inter alia, in that often a view minutes after the production of the vaccine composition, individual components sediment in the generally liquid preparations.
  • those vaccine compositions in which adjuvant and antigen are immobilised on different aluminium salt particles, such as, for example, the composition which is described in WO-A-00/23105, only have a low immune stimulatory effect.
  • the process described in WO-A-00/23105 requires the use of at least two separate stirring vessels, in which the aluminium salt particle-antigen composition, as well as the aluminium salt particle-adjuvant composition is prepared.
  • a further disadvantage of the vaccine compositions known from the prior art are the often pronounced variations in the immune stimulatory effect of the vaccine compositions between individual production batches.
  • the present invention had the object of overcoming the disadvantages of vaccine compositions known from the prior art, in particular of vaccine compositions for prevention of a hepatitis B illness.
  • the present invention had the object of providing a process for pro- duction of a vaccine composition, which enables the production of a vaccine composition with, to the greatest extent possible, more constant and batch- independent immune stimulatory effect. It should be possible to carry out this process as much as possible with a single stirring vessel, into which the individual components can be introduced, and still enable the production of vaccine compo- sition with a high immune stimulatory effect.
  • the present invention also had the object of providing a process for production of a vaccine composition, which enables the production of vaccine compositions which are as storage-stable as possible.
  • a contribution to the solution of the above-mentioned objects is made by a process for production of a vaccine composition, comprising as process steps:
  • the aqueous phase Pi comprises, preferably before the process step iii), less than 10 mg/ml aluminium;
  • the aqueous phase P 2 comprises less than 1 mg/ml of the antigen; d) the volume V 2 is added with a rate of at most 10% of the amount of the volume Vi/minute to volume V 1 .
  • Preferred embodiments according to the invention of the process according to the invention are those processes in which the following properties or combinations of properties are fulfilled: a), b), c), d), a)b), a)c), a)d), b)c), b)d), c)d), a)b)c), a)b)d), a)c)d), b)c)d) and a)b)c)d), whereby a), b)c)d) and a)b)c)d) are particularly preferred and a)b)c)d) is most preferred.
  • aqueous phase P 1 comprising an aluminium compound whose surface has to brought into contact with phosphate ions.
  • This aqueous phase P 1 can be, depending on the aluminium compound comprised, an aqueous solution, an aqueous dispersion, an aqueous emulsion or an aqueous suspension.
  • aqueous should merely mean that the corresponding phase comprises water as solvent or as part of a solvent mixture.
  • Preferred aluminium compounds comprise compounds selected from the group consisting of aluminium sulphate, aluminium chloride, aluminium hydroxide, in particular aluminium orthohydroxides, such as, for example, hydrargillite ( ⁇ - Al(OH) 3 , bayerite ( ⁇ -Al(0H) 3 ) or Nordstrandite ( ⁇ -Al(OH) 3 ), aluminium meta- hydroxides, such as, for example, bohmite ( ⁇ - Al(O)OH), which is commercially obtainable, for example under the name Alhydrogel ® or Rehydragel ® or diaspor ( ⁇ -Al(O)OH), aluminium phosphates, such as, for example, AlPO 4 or amorphous aluminium hydroxyphosphate gel (Al(OH) m (PO 4 ) n ), such as is commercially obtainable, for example under the name AdjuPhos ® or RehydraPhos ® , as well as mixed oxides between aluminium and further metals, in particular between aluminium and
  • aluminium metal hydroxides are obtainable commercially in crystalline form.
  • aluminium compounds compris ⁇ ing mixtures of at least two of the above-mentioned compounds conceivable, for example, mixtures comprising aluminium phosphate and aluminium hydroxide, in particular mixtures comprising aluminium hydroxyphosphate gel and Al(O)OH.
  • the aluminium compound in the vaccine composition according to the invention is preferably present in particulate form, whereby it is particularly preferred in this connection that at least 75 %, yet more preferably at least 85 % and most preferably at least 95 % of the particles, respectively based on the number of particles, are smaller than 2 ⁇ m. It is furthermore preferred in this context that the particles of the aluminium compound preferably have a size in a range from 0.5 to 15 ⁇ m, particularly preferably
  • the surface of the aluminium compound provided in process step i) has been brought into contact with phosphate ions.
  • the aluminium compound is dissolved or dispersed, preferably dispersed, in an aqueous phase P 1 , which comprises a preferably water-soluble salt of a phosphate, whereby the salt of a phosphate is preferably selected from the group comprising sodium phosphate, sodium dihydrogenphosphate, disodium hydrogenphosphate, potassium phosphate, dipotassium hydrogenphosphate, potassium dihydrogenphosphate or mixtures of at least two of these phosphates, whereby mixtures of disodium hydrogenphosphate and sodium dihydrogenphosphate are most preferred.
  • PBS phosphate buffered saline
  • disodium or dipotassium hydrogenphosphate which is preferably present in a concentration in a range from 1 to 10 mM, particularly preferably from 3 to 8 mM and most preferably of about 5 mM
  • sodium or potassium dihydrogenphosphate which is preferably present in a concentration in a range from 1 to 10 mM, particularly preferably from 3 to 8 mM, and most preferably of about 5 mM, as well as
  • NaCl which is preferably present in a concentration in a range from 125 to 175 mM, particularly preferably from 140 to 160 mM and most preferably in a concentration of about 150 mM.
  • the pH-value of the aqueous phase Pi, in particular of the PBS buffer lies, at 25 0 C, preferably in a range from 6 to 8, particularly preferably from 6.5 to 7.5.
  • a 1.5* to 6 ⁇ PBS buffer particularly preferably a 1.75 x to 5 ⁇ PBS buffer and most preferably a 2 ⁇ to 4 ⁇ PBS buffer is used, whereby a 2 ⁇ to 4 ⁇ PBS buffer comprises the above-mentioned concentrations of sodium chloride, disodium or dipotassium hydrogenphosphate and sodium or potassium dihydrogenphosphate in two times to four times the amount of those concentrations which where given above as preferred, particularly preferred and most preferred concentrations for the individual components.
  • a 1.5xPBS buffer comprises
  • disodium or dipotassium hydrogenphosphate preferably in a concentration in a range from 1.5 to 15 mM, particularly preferably from 4.5 to 12 mM and most preferably of about 7.5 mM
  • sodium or potassium dihydrogenphosphate preferably in a concentration in a range from 1.5 to 15 mM, particularly preferably from 4.5 to 12 mM and most preferably of about 7.5 mM
  • disodium or dipotassium hydrogenphosphate preferably in a concentration in a range from 1.5 to 15 mM, particularly preferably from 4.5 to 12 mM and most preferably of about 7.5 mM
  • - NaCl preferably in a concentration in a range from 187.5 to 262.5 mM, particularly preferably from 210 to 240 mM and most preferably in a concentration of about 225 mM.
  • a 2x to 4> ⁇ PBS buffer is provided, in which an aluminium metal hydroxide, in particular the aluminium compound obtainable under the name Alhydrogel , is dispersed.
  • the aluminium compound is heated after the bringing into contact with the phosphate ions and before process step iii), whereby this heating preferably occurs to a temperature of at least 100 0 C, preferably of at least 11O 0 C, and most preferably of at least 120 0 C, preferably to a temperature in a range from 100 to 150 0 C, particularly preferably to a temperature in a range from 110 to 14O 0 C and most preferably to a temperature in a range from 120 to 130 0 C.
  • the duration of the heating to a temperature within the above-mentioned temperature ranges is generally at least 10 minutes, particularly preferably at least 15 minutes and most preferably at least 20 minutes, whereby, advantageously, a duration of 4 hours, particularly preferably of 2 hours, is not exceeded. It can, furthermore, be advantageous to stir the aqueous phase P t during the heating, in order to ensure as homogeneous as possible a bringing into contact of the surface of the aluminium compound with the phosphate ions. Subsequently to the heating, the hot aqueous phase P 1 is allowed to cool, preferably to a temperature in a range from 15 to 40 0 C, particularly preferably to a temperature in a range from 18 to 24°C.
  • a dilu ⁇ tion step can follow the heating of this PBS solution, in which the concentrated PBS solution is optionally diluted with deionised or distilled water, preferably until the concentration of the PBS buffer reaches the concentration of Ix to 2 ⁇ PBS, especially preferred 1.3x to 1.7xPBS.
  • the aqueous phase P 1 comprises, after the heat- ing, if this is carried out, and particularly after an optionally carried out dilution step, less than 10 mg/ml aluminium, particularly preferably less than 5 mg/ml, yet more preferably less than 2.5 mg/ml and most preferably less than 1 mg/ml aluminium.
  • a volume V 2 of an aqueous phase P 2 comprising an antigen is provided.
  • the aqueous phase P 2 can also be, depending on the antigen comprised, an aqueous solution, an aqueous dispersion, an aqueous emulsion or an aqueous suspension.
  • Preferred antigens are selected from the group comprising antigens or antigen compositions from the HIV-I -virus, for example, tat, nef, gpl20 or gpl60 antigens or antigen compositions from the from humane herpes virus, for example, gD or derivatives thereof, so-called Immediate Early Proteins such as, for exam- pie, ICP27 from HSV-I or HSV-2, antigens or antigen compositions from the cytomegalo- virus, such as, gB or derivatives thereof, antigens or antigen compositions from the rota-virus, antigens or antigen compositions from the Epstein-Barr- Virus, such as, for example, gp350 or derivatives thereof, antigens or antigen compositions from the Varicella-Zoster- Virus, such as, for example, gpl, gpll or IE63, antigen or antigen compositions from hepatitis- virus, in particular from the Hepatit
  • iS. pneumonie for example H. influenzae npe B, non-typable H. influenzae, H. ducreyi, Moraxella spp.
  • M. catarrhalis also known as Branhamella catarrhalis, Borde- tella s
  • bronchiseptica Mycobacterium spp., in particular M. tuberculosis, M. bonis, M. leprae, M. avium, M. paratuberculosis, M. smegmatis, Legionella spp., in particular L. pneumophila, Escherichia spp., in particular enterotoxic E. coli, enterohemorrhagic E. coli or enteropathogenic E. coli, Vibrio spp., in particular V. cholera (for example the Cholera-Toxin or de- rivatives thereof) Shigella spp., in particular S. sonnei, S. dysenteriae oder S.
  • V. cholera for example the Cholera-Toxin or de- rivatives thereof
  • Shigella spp. in particular S. sonnei, S. dysenteriae oder S.
  • flex- nerii Yersinia spp., in particular Y. enterocolitica, Y. pestis, Y. pseudotuberculosis, Campylobacter spp., in particular C. jejuni or C. coli, Salmonella spp., in particular S. typhi, S. paratyphi, S. choleraesuis or S. enteritidis, Listeria spp., in particular L. monocytogenes, Helicobacter spp., in particular H pylori, Pseudomonas spp., in particular P. aeruginosa, Staphylococcus spp., in particular S. aureus or S.
  • Clostridium spp. in particular C. tetani (for example the Tetanus-Toxin and derivatives thereof), C. botulinum (for example the Botulinum-Toxin or derivatives thereof), C. difficile (for example the Clostridium-Toxin A or B or derivatives thereof), Bacillus spp., in particular B. anthracis, Corynebacterium spp., in particular C. diphtheriae (for example the Diphtherie-Toxin and derivatives thereof), Borrelia spp., in particular B. burgdorferi, B.
  • Toxoplasma spp. in particular T. gondii, Entamoeba spp., in particular E. histolytica, Babesia spp., in particular B. microti, Trypanosoma spp., in particular T. cruzi, Giardia spp., in particular G. lamblia, Leshmania spp., in particular L. major, Pneumocystis spp., in particular P. carinii, Trichomonas spp., in particular T. vaginalis, Schisostoma spp., in particular S. mansoni, or antigens or antigen compositions from yeasts, for example Candida spp., in particular C. albicans, or Cryptococcus spp., in particular C. neoformans.
  • the antigen is the HBsAg, a fragment of this antigen, a variant of this antigen or of the fragment of this antigen or a mixture of at least two thereof.
  • fragment of a HBsAg is preferably understood a polypeptide, in which a section of at least 25, preferably at least 50 and particu- larly preferably at least 100 amino acids is identical with a corresponding section of the HBsAg, while, by the term “variant" of the HBsAg or of the fragment of the HBsAg, preferably is understood a polypeptide, in which at most 10, preferably at most 5 amino acids, particularly preferably at most 2 amino acids and most preferably at most 1 amino acid of the HBsAg or the fragment of the HBsAg is, or are deleted, inserted, substituted or attached at the C- and/or N-terminal ends.
  • variant also comprises fusion polypeptid
  • HBsAg is a 226 amino acid protein (p24/gp27 or S-protein), which self-assembles in 20-30 ran lipoprotein particles, in which approximately 100-150 sub-units are cross-networked by means of multiple inter-and intra-molecular disulfide bonds.
  • the HBsAg's can be derived from eight presently known HBV-standard genotypes A, B, C, D, E, F, G and H. These eight standard genotypes differ in approximately 8 % of their nucleotide sequence (see Bartholomeusz, Rev. Med. Virol. 13 (2003), 1-14), whereby the variation concerns above all the HBsAg-Gen.
  • the HBV genotype A has the reference nucleic acid sequence Genbank X02763 or the HBV genotype A 3 ⁇ has the reference nucleic acid sequence according to Genbank AF297621.
  • the reference nucleic acid sequence is Genbank D00330, for the genotype Bj, the reference nucleic acid sequence AB073858.
  • the reference nucleic acid sequence is Genbank AY206389, for the genotype C aUs> the reference nucleic acid sequence according to Genbank AB048704.
  • the reference nucleic acid sequence is Genbank X02496, for the genotype E Genbank X75657, for the genotype F Genbank X69798, for the genotype G Genbank AFl 60501 and for the genotype H Genbank AY090454.
  • HBsAg further comprises, in addition to the 226 amino acid protein, also the two M- and L-proteins, which further comprise, in addition to the HBsAg, the 55 amino acid-long pre-S2-peptide (M-protein) or the 55 amino acid-long pre- S2-peptide and the 120 amino acid long pre-Sl -peptide (L-protein).
  • the aqueous phase P 2 comprises not only a HBsAg, but also, as described in WO-A-2005/02397, at least two HBsAg's or fragments or variants thereof, whereby the HBsAg differ in the HBV genotype in the S-region and/or in the pre- Sl -region.
  • the HBsAg and/or the HBsAg's can be obtained either from the serum of patients with chronic hepatitis B, in synthetic ways, or as recombinant polypeptides by means of processes known to the skilled person.
  • a possibility for the production of HBsAg as recombinant polypeptide consists in amplifying the core or pre-core reading frame by means of polymerase chain reaction (PCR) of a virus isolate. It is also conceivable to produce the corresponding DNA-sequence in a synthetic way and then to amplify by means of PCR. The ob- tained PCR-fragment is then cloned in a plasmid vector.
  • PCR polymerase chain reaction
  • the fragment can then be inserted into an expression vector, for example into an expression vector for E. coli.
  • the insertion preferably occurs in such a way that the gene coding for the HBsAg or for the fragment of the variant is under the control of an active promoter.
  • the expression vector can at the same time comprise induction elements for increasing the expression rate.
  • individual clones are obtained, which express the HBsAg or the fragment or the variant.
  • an individual clone is injected in culture medium and cultivated over night at 37°C in the shaking flask. The E. coli culture is then first harvested by centrifugation.
  • the bacteria pellet is resuspended in buffer solution and then disrupted by ultrasound treatment or by high pressure homogenisation.
  • the HBsAg or HBsAg variants respectively located in the ho- mogenisat is concentrated by precipitation with ammonium sulphate and then purified of bacterial host components by gel filtration.
  • the HBsAg or respectively fragments thereof or variants thereof comprised in the composition according to the invention can also be obtained in a synthetic way.
  • HBsAg Recombinant hepatitis B vaccines: disease characterization and vaccine production” (2005) in Gellissen G (editor): production of recombinant proteins - novel microbial and eucaryontic expression systems", pages 319-360, Wiley- VCH, Weinheim).
  • HBsAg can also be commercially obtained, for example, from the company Rhein Biotech GmbH, D ⁇ sseldorf.
  • the aqueous phase P 2 is buffered by means of a suitable buffer system, for example, by means of the PBS buffer described in connection with the aqueous phase P 1 , whereby, contrary to the aqueous phase P 1 , the aqueous P 2 comprising the antigen is preferably present as IxPBS buffer.
  • an antigen stock solution is prepared, which is then diluted with a buffer solution, preferably with a 1 xPBS buffer.
  • the thus-obtained solution can then be sterilised, before it is added to aqueous phase P 1 in process step iii), whereby this sterilisation preferably occurs by means of sterile filtration.
  • the aqueous phase P 2 comprises less than 2 mg/ml, preferably less than 1 mg/ml, particularly preferably less than 0.5 mg/ml, yet more preferably less than 0.3 mg/ml and most preferably less than 0.2 mg/ml of the antigen.
  • step iii) of the process according to the invention for production of a vaccine composition the volume V 2 of the aqueous phase P 2 is now added to the volume V 1 of the aqueous phase P 1 with stirring of the volume Vi, whereby, preferably, first the volume V 1 of the aqueous phase P 1 is provided with stirring, and then, successively the volume V 2 of the aqueous phase P 2 is stirred into the volume Vi of the aqueous phase P 1 .
  • the aluminium metahydroxide in which aluminium metahydroxide is used as aluminium compound, first, as described above, the aluminium metahydroxide, in a 1.5* to 6 ⁇ PBS buffer, particularly preferably in a 1.75* to 5*PBS buffer and most preferably in a 2x to 4 ⁇ PBS buffer is provided, with stirring, then heated, with stirring, at the above- described temperature and for the above-described duration, afterwards cooled to the above-described temperature, optionally diluted with water, preferably until the concentration of the PBS buffer reaches the concentration of Ix to 2 ⁇ PBS, especially preferred 1.3 ⁇ to IJxPBS, and the volume V 2 of the aqueous phase P 2 stirred into the thus-obtained volume V) of the aqueous phase P 1 .
  • volume V 2 is added to volume Vj.
  • the volume V 2 is added with a rate of at most 2 litre/minute, particularly preferably of at most 1 litre/minute, yet more preferably of at most 0.5 litre/minute and most preferably of at most 0.2 litre/minute, whereby the addition of the volume V 2 to the volume V 1 preferably occurs with continuous stirring of the volume V 1 .
  • the amount of the vol- ume V 2 is about 10 to 50 %, preferably about 15 to 40 % and most preferably about 20 to 30 % of the amount of the volume Vj.
  • the process additionally comprises the following process step: iv) provision of a volume V 3 of an aqueous phase P 3 comprising an adjuvant different to the aluminium compound,
  • the aqueous phase P 3 comprises less than 1 mg/ml of the adjuvant
  • the volume V 3 is added with a rate of at most 10 % of the amount of the volume Vi/minute to the volume V 1 , of at most 10 % of the amount of vol- ume V 2 /minute to the volume V 2 or respectively of at most 10 % of the amount of the volume of the mixture of the volumes Vi and V 2 /minutes to the mixture of the volumes Vi and V 2 , preferably, however, of at most 10 % of the amount of the volume of the mixture of the volumes V 1 and V 2 /minute, to the mixture of the volumes Vi and V 2 .
  • Embodiments preferred according to the invention of this in turn preferred embodiment of the process according to the invention are those processes, in which the following properties or combinations of properties are fulfilled: a)e), a)f), b)e), b)f), c)e), c)f), d)e), d)f), a)e)f), b)c)d)e)f) and a)b)c)d)e)f), whereby a), b)c)d)e)f) and a)b)c)d)e)f) are particularly preferred and a)b)c)d)e)f) is most preferred.
  • a volume V 3 of an aqueous phase P 3 of an adjuvant different to the aluminium compound is prepared, whereby the aqueous phase P 3 , just as with the aqueous phases P 1 and P 2 , can be an aqueous solution, an aqueous dispersion, an aqueous emulsion or an aqueous suspension.
  • the adjuvant which is comprised in the aqueous solution can be any adjuvant known to the skilled person which is commonly used in vaccine compositions.
  • adjuvant is understood a compound which enables the induction of an immune response, preferably the induction of a cellular immune response to the antigen comprised in the aqueous phase P 2 .
  • Adjuvants preferred according to the invention and different from aluminium compounds are selected in particular from the group comprising aluminium-free, particulate adjuvants, such as, for example, sub-micron-oil-in-water emulsion, to which belong, for example, MF59 (5 % Squalene, 0,5 % Tween ® 80 and 0,5 % Span ® 85), SAF (10 % Squalene, 0,4 % Tween ® 80, 5 % pluron-blocked polymer as well as thr-muramyldipeptide (thr-MDP)), incomplete Freundsches adjuvant, lipopolysaccharides, N-Acetylglucosaminyl-N-acetylmuramyl-L-alanyl-dipeptide (GMDP) or muramyldipeptide (MDP), Gal-ceramide, dimethyldiocta- decylammonium bromide (DDAB), liposomes
  • adjuvants are lipopolysaccharides, Gal-ceramides, oligodesoxyribonucleotides with CpG-motif, PEG-sorbitan fatty acid esters, a Saponin- or a Saponin derivative-comprising adjuvant, such as, for example, the commercially obtainable products AbISCO - 100, AbISCO ® -200, AbISCO ® -300 (ISCONOVA, Uppsala, Sweden) or Stimu- lon ® QS-21 (ANTIGENICS, Woburn, USA), as well as 3-0-deacetylated mono- phosphoryl-lipid A.
  • aqueous phase P 3 comprising the adjuvant
  • this is buffered by means of a suit- able buffer system, for example by means of the PBS buffer described in connection with the aqueous phases P 1 and P 2 , whereby, contrary to the aqueous phase Pj and in agreement with the aqueous phase P 2 , the aqueous P 3 comprising the adjuvant preferably is present as a 1 *PBS buffer.
  • an adjuvant stock solution is provided, which is then diluted with a buffer solution or with deionised or distilled water, preferably with deionised or distilled water.
  • the thus-obtained aqueous phase P 3 can then be sterilised, whereby this sterilisa- tion preferably occurs by means of sterile filtration.
  • the aqueous phase P 3 comprises less than 1 mg/ml, preferably less than 0.75 mg/ml, particularly preferably less than 0.5 mg/ml, yet more preferably less than 0.3 mg/ml and most preferably less than 0.15 mg/ml of the adjuvant.
  • the volume V 3 of the aqueous phase P 3 is now added to the volume V 1 of the aqueous phase P 1 , to the volume V 2 of the aqueous phase P 2 or to the mixture of the volumes Vi and V 2 obtained in process step iii), preferably, however, to the mixture of volumes V 1 and V 2 obtained in process step iii).
  • the volume V 3 is added, with a rate of at most 10 %, particularly preferably of at most 5 %, yet more preferably of at most 2.5 % and most preferably of at most 1 % of the amount of the volume V 1 , of the amount of the volume V 2 or of the amount of the mixture of volumes V 1 and V 2 /minute to the volume V 1 , to the volume V 2 or re- spectively to the mixture of volumes Vi and V 2 .
  • the volume V 3 of the aqueous phase P 3 is about 20 to 70 %, particularly preferably about 30 to 60 % and most preferably about 40 to 50 % of the volume V 1 of the aqueous phase P ⁇ .
  • the process according to the invention can also comprise further process steps, in particular a process step vi), in which to the volume Vi, to the volume V 2 , to the volume V 3 , to the mixture of volumes V 1 and V 2 , to the mixture of the volumes V 1 and V 3 , to the mixture of the volumes V 2 and V 3 , to the mixture of the volumes V 1 , V 2 and V 3 , particularly preferably, however, to the mixture of the volumes V 1 , V 2 and V 3 , a further volume V 4 of a preferably aqueous and preferably sterile phase P 4 comprising one or more additives, for example, antioxidants, buffer components, colouring agents, viscosity regulators or preservatives is added.
  • a process step vi in which to the volume Vi, to the volume V 2 , to the volume V 3 , to the mixture of volumes V 1 and V 2 , to the mixture of the volumes V 1 and V 3 , to the mixture of the volumes V 2 and V 3 , to the mixture of the volumes V 1
  • the antigen is immobilised homogeneously on the substrate.
  • aluminium compound and as antigen those compounds and components re- spectively are preferred which have already been mentioned above in connection with the process according to the invention for production of a vaccine composition as preferred antigens and aluminium compounds respectively.
  • a “homogeneous” immobilisation of the antigen on the substrate is preferably understood an immobilisation which, with an immunohistochemical colouring of the vaccine composition according to the invention by means of FITC- or TRITC- marked monoclonal antibodies which are directed against to the respective antigen, allow to recognise a homogeneous colouration of the substrate surface.
  • this additionally comprises III) an adjuvant, which is likewise immobilised on the substrate,
  • adjuvant is likewise immobilised homogeneously on the substrate.
  • adjuvant are likewise preferred those compounds or components which have already been described as preferred adjuvants in connection with the process according to the invention for production of a vaccine composition.
  • a further contribution to the solution of the above-mentioned objects is also made by the use of the vaccine composition obtainable by the process according to the invention or of the vaccine composition according to the invention for the production of a pharmaceutical for prophylaxis or therapy, preferably prophylaxis, of viral illnesses, in particular the use of the vaccine composition comprising HBsAg as antigen as vaccine for the prophylaxis or therapy, preferably prophylaxis, of a hepatitis B illness in humans.
  • prophylaxis in connection with HBV-infection in humans preferably comprises
  • the therapeutically effective dose for the respective application case depends, for example, on the exact composition of the vaccine composition according to the invention or respectively of the pharmaceutical according to the invention, the method of administration as well as the weight and the general state of health of the patient, but generally lies preferably in a range from about 0.1 to 2,000 ⁇ g (total amount of aluminium compound, antigen and optionally adjuvant) for a 70 kg patient, particularly preferably in a range from 0.5 to 1,500 ⁇ g, yet more preferably in a range from 1 to 1,000 ⁇ g and most preferably in a range from 10 to 500 ⁇ g, whereby the vaccine composition according to the invention preferably is administered in the form of merely 2 doses, preferably administered at a separation of 2 weeks to 2 months, particularly preferably at a separation of about one month.
  • the vaccine composition according to the invention or respectively the pharma- ceutical according to the invention can, in principal, be administered orally, intra- nasally, subcutaneously, intramuscularly or intravenously.
  • a further contribution to the solution of the above-mentioned object is made by a process for immunisation of a human, whereby the vaccine composition obtain- able by the process according to the invention, the vaccine composition according to the invention or the pharmaceutical is administered to a patient, preferably to a human, preferably in the form of a first and second doses, whereby the separation between the first and second dose is preferably 2 weeks to months, preferably about one month.
  • the invention is now more closely illustrated by means of a non-limiting exam ⁇ ple.
  • aluminium metahydroxide gel (Alhydrogel ® , Brenntag Biosector,
  • HBsAg (Rhein Biotech GmbH, D ⁇ sseldorf) is diluted with PBS (comprises about 0.98 mg/ml disodium hydrogenphosphate dihydrate, 0.71 mg/ml sodium dihydrogenphosphate dihydrate and 9 mg/ml sodium chloride) to a concentration of about 0.1 mg/ml.
  • PBS disodium hydrogenphosphate dihydrate, 0.71 mg/ml sodium dihydrogenphosphate dihydrate and 9 mg/ml sodium chloride
  • aqueous phase P 1 total volume about 18 litres
  • aqueous phase P 2 total volume about 4.4 litres
  • the thus-obtained vaccine composition was characterised by an excellent immu- nogenity and stability.

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Virology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Immunology (AREA)
  • Medicinal Chemistry (AREA)
  • Microbiology (AREA)
  • Mycology (AREA)
  • Chemical & Material Sciences (AREA)
  • Epidemiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Communicable Diseases (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)

Abstract

La présente invention concerne un procédé de production d'une composition vaccinale consistant (i) à obtenir un volume V1 d'une phase aqueuse P1 comprenant un composé d'aluminium dont la surface a été mise en contact avec des ions phosphate, (ii) à obtenir un volume V2 d'une phase aqueuse P2 d'un antigène, et (iii) à ajouter le volume V2 de la phase aqueuse P2 au volume V1 de la phase aqueuse P1 avec agitation du volume V1, l'une au moins, de préférence chacune, des conditions suivantes étant remplie: (a) le composé d'aluminium est chauffé après sa mise en contact avec les ions phosphate et avant l'étape (iii), (b) la phase aqueuse P1 comprend moins de 10 mg/ml d'aluminium, (c) la phase aqueuse P2 comprend moins de 1 mg/ml de l'antigène, et (d) le volume V2 est ajouté à une vitesse d'au moins 10% la quantité du volume V1 par minute au volume V1. L'invention concerne également la composition vaccinale pouvant être obtenue au moyen de ce procédé, une composition vaccinale comprenant un substrat et un antigène ainsi que l'utilisation d'une composition vaccinale.
PCT/EP2007/004819 2006-05-31 2007-05-31 Procédé de production d'une composition vaccinale WO2007137847A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP20060011345 EP1862176A1 (fr) 2006-05-31 2006-05-31 Procédé de production de composition vaccinale
EP06011345.3 2006-05-31

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WO2007137847A1 true WO2007137847A1 (fr) 2007-12-06

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993024148A1 (fr) * 1992-05-23 1993-12-09 Smithkline Beecham Biologicals (S.A.) Vaccins combines contenant des antigenes de surface du virus de l'hepatite b et d'autres antigenes
WO1996026741A1 (fr) * 1995-02-25 1996-09-06 Smithkline Beeecham Biologicals S.A. Vaccin a l'hepatite b
WO1999048525A1 (fr) * 1998-03-25 1999-09-30 Smithkline Beecham Biologicals S.A. Composition de vaccin contre hib/dtpa et ses methodes de preparation
WO1999056772A2 (fr) * 1998-05-01 1999-11-11 Smithkline Beecham Biologicals S.A. Nouvelle composition
WO2003066094A2 (fr) * 2002-02-07 2003-08-14 Glaxosmithkline Biologicals S.A. Nouveau vaccin
WO2006087563A2 (fr) * 2005-02-16 2006-08-24 Novartis Vaccines And Diagnostics, Inc. Composition d'adjuvant comprenant du phosphate d'aluminium et 3d-mpl

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993024148A1 (fr) * 1992-05-23 1993-12-09 Smithkline Beecham Biologicals (S.A.) Vaccins combines contenant des antigenes de surface du virus de l'hepatite b et d'autres antigenes
WO1996026741A1 (fr) * 1995-02-25 1996-09-06 Smithkline Beeecham Biologicals S.A. Vaccin a l'hepatite b
WO1999048525A1 (fr) * 1998-03-25 1999-09-30 Smithkline Beecham Biologicals S.A. Composition de vaccin contre hib/dtpa et ses methodes de preparation
WO1999056772A2 (fr) * 1998-05-01 1999-11-11 Smithkline Beecham Biologicals S.A. Nouvelle composition
WO2003066094A2 (fr) * 2002-02-07 2003-08-14 Glaxosmithkline Biologicals S.A. Nouveau vaccin
WO2006087563A2 (fr) * 2005-02-16 2006-08-24 Novartis Vaccines And Diagnostics, Inc. Composition d'adjuvant comprenant du phosphate d'aluminium et 3d-mpl

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
GUPTA R K ET AL BORCHARDT R T (ED ): "ADJUVANT PROPERTIES OF ALUMINUM AND CALCIUM COMPOUNDS", 1995, VACCINE DESIGN. SUBUNIT AND ADJUVANT APPROACH, PHARMACEUTICAL BIOTECHNOLOGY, NEW YORK, PLENUM PRESS, US, PAGE(S) 229-248, ISBN: 0-306-44867-X, XP002925125 *
R.K. GUPTA & B.E. ROST (ED): "METHODS IN MOLECULAR MEDICINE, VOL. 42: VACCINE ADJUVANTS: PREPARATION METHODS AND RESEARCH PROTOCOLS", 2000, HUMANA PRESS INC, TOTOWA, NJ, USA, XP002405902 *
ULRICH J T ET AL BORCHARDT R T (ED ): "MONOPHOSPHORYL LIPID A AS AN ADJUVANT", 1995, VACCINE DESIGN. SUBUNIT AND ADJUVANT APPROACH, PHARMACEUTICAL BIOTECHNOLOGY, NEW YORK, PLENUM PRESS, US, PAGE(S) 495-526, ISBN: 0-306-44867-X, XP000942421 *

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EP1862176A1 (fr) 2007-12-05

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